EP3009180A1 - Apparatus and method for treating harmful gases and preventing generation of and removing harmful substances - Google Patents

Apparatus and method for treating harmful gases and preventing generation of and removing harmful substances Download PDF

Info

Publication number
EP3009180A1
EP3009180A1 EP14810303.9A EP14810303A EP3009180A1 EP 3009180 A1 EP3009180 A1 EP 3009180A1 EP 14810303 A EP14810303 A EP 14810303A EP 3009180 A1 EP3009180 A1 EP 3009180A1
Authority
EP
European Patent Office
Prior art keywords
primary
harmful
cooling water
harmful gases
gases
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP14810303.9A
Other languages
German (de)
French (fr)
Inventor
Woong Hoe Kim
See Woong KIM
Sang Guk JEON
Soo Yong Jung
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sinyoung Construction Co Ltd
Original Assignee
Sinyoung Construction Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sinyoung Construction Co Ltd filed Critical Sinyoung Construction Co Ltd
Publication of EP3009180A1 publication Critical patent/EP3009180A1/en
Withdrawn legal-status Critical Current

Links

Images

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/02—Separating dispersed particles from gases, air or vapours by liquid as separating agent by passing the gas or air or vapour over or through a liquid bath
    • B01D47/021—Separating dispersed particles from gases, air or vapours by liquid as separating agent by passing the gas or air or vapour over or through a liquid bath by bubbling the gas through a liquid bath
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/02—Separating dispersed particles from gases, air or vapours by liquid as separating agent by passing the gas or air or vapour over or through a liquid bath
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/16—Apparatus having rotary means, other than rotatable nozzles, for atomising the cleaning liquid
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/18—Absorbing units; Liquid distributors therefor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/46—Removing components of defined structure
    • B01D53/72—Organic compounds not provided for in groups B01D53/48 - B01D53/70, e.g. hydrocarbons
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/75—Multi-step processes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/77—Liquid phase processes
    • B01D53/78—Liquid phase processes with gas-liquid contact
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20—Mixing gases with liquids
    • B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/233—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/91—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with propellers
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/02—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
    • F01N3/037—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of inertial or centrifugal separators, e.g. of cyclone type, optionally combined or associated with agglomerators
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2247/00—Details relating to the separation of dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D2247/04—Regenerating the washing fluid
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2251/00—Reactants
    • B01D2251/30—Alkali metal compounds
    • B01D2251/304—Alkali metal compounds of sodium
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2251/00—Reactants
    • B01D2251/60—Inorganic bases or salts
    • B01D2251/604—Hydroxides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/70—Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2258/00—Sources of waste gases
    • B01D2258/02—Other waste gases
    • B01D2258/025—Other waste gases from metallurgy plants
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2258/00—Sources of waste gases
    • B01D2258/02—Other waste gases
    • B01D2258/0283—Flue gases
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2258/00—Sources of waste gases
    • B01D2258/02—Other waste gases
    • B01D2258/0283—Flue gases
    • B01D2258/0291—Flue gases from waste incineration plants
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20—Mixing gases with liquids
    • B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/233—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements
    • B01F23/2336—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the location of the place of introduction of the gas relative to the stirrer
    • B01F23/23363—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the location of the place of introduction of the gas relative to the stirrer the gas being introduced above the stirrer
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00—Road transport of goods or passengers
    • Y02T10/10—Internal combustion engine [ICE] based vehicles
    • Y02T10/12—Improving ICE efficiencies

Definitions

  • This invention relates to an apparatus and method for treating harmful gases and preventing generation of and removing harmful substances, and more particularly, to an apparatus and method for treating harmful gases and preventing generation of and removing harmful substances, which rapidly cools the harmful gases and thus fundamentally prevents the generation of and removes harmful substances such as dioxins.
  • Exhaust gases generated from an incinerator which incinerates household garbage of cities or industrial waste contain harmful substances such as CO 2 , HCl, NO x , So x , dust and dioxins.
  • harmful substances such as CO 2 , HCl, NO x , So x , dust and dioxins.
  • Various conventional methods for treating the exhaust gases containing the above-described harmful substances have been used.
  • Such conventional technologies for preventing emission of the harmful substances cause many problems such as the wide installation area due to an increase in a size of a facility for preventing the emission of the harmful substances and high investment costs.
  • the high costs cause a rise in manufacturing cost, and thus lead to a serious problem in price competitiveness of production goods, and particularly, provide a big worry to many companies which are confronted with regulations relative to greenhouse gas emission.
  • the present invention is directed to providing an apparatus and method for treating harmful gases and preventing generation of and removing harmful substances, which fundamentally prevents generation of harmful substances from harmful gases, and thus simplifies a harmful gas treatment process.
  • the present invention is directed to providing an apparatus and method for treating harmful gases and preventing generation of and removing harmful substances, which has a simple structure and thus minimizes costs for installation and management of a facility.
  • the present invention is directed to providing an apparatus and method for treating harmful gases and preventing generation of and removing harmful substances, which is able to prevent the generation of the harmful substances by rapidly cooling high temperature harmful gases, and also, to prevent the generation of the harmful substances from the harmful gases, which does not have high temperature, through treatment water, and thus to be selectively used according to a generation process of the harmful gases.
  • One aspect of the present invention provides an apparatus and method for treating harmful gases and preventing generation of and removing harmful substances, including a primary prevention processing part connected with a flue in which harmful gases and harmful substances generated by high temperature flame flow and configured to rapidly cool the harmful gases to prevent the harmful substances from being produced from the harmful gases, wherein the primary prevention processing part includes a primary processing chamber in which cooling water is accommodated; a primary suction pipe which is provided inside the primary processing chamber and connected with the flue; a primary rotary blade part which is coupled to a lower portion of the primary suction pipe, rotated in a submerged state under the cooling water, discharges the harmful gases in the form of microbubbles into the cooling water to allow the harmful gases to come into contact with the cooling water and to be rapidly cooled; and a primary rotary blade driving part which rotates the primary rotary blade part.
  • the primary suction pipe may be formed to have an outer diameter corresponding to an inner diameter of the flue, and may be provided so that an upper end thereof is inserted into the flue to a predetermined length and a lower end thereof is in communication with the primary rotary blade part.
  • the primary rotary blade part may include a harmful gas suction pipe where an upper portion is opened so as to be in communication with the primary suction pipe, and an outer circumferential surface having harmful gas discharge ports formed at regular intervals; an upper support plate and a lower support plate which are coupled to an upper portion and a lower portion of the harmful gas suction pipe, respectively; and a plurality of rotary blades which are spirally coupled at one sides of the harmful gas discharge ports and discharge the harmful gases to the cooling water.
  • Ends of the rotary blade may be formed to protrude outward to a predetermined length in radial directions of the upper support plate and the lower support plate.
  • a cooling water circulation and filtration part which circulates the cooling water therein and discharges sludge is provided at one side of the primary processing chamber.
  • the apparatus may further include a secondary prevention processing part which dissolves primarily treated gases treated in the primary prevention processing part in treatment water in which a harmful gas treatment agent dissolved, and treats residual substances contained in the primarily treated gases.
  • the object of the present invention can be achieved by the apparatus and method for treating the harmful gases and preventing the generation of and removing the harmful substances.
  • Another aspect of the present invention provides a method for treating harmful gases and preventing generation of and removing harmful substances, including a primary treatment operation in which the apparatus for treating the harmful gases and preventing the generation of and removing the harmful substances is coupled to a flue in which the high temperature harmful gases flow, rapidly cools the harmful gases by bringing the harmful gases into contact with cooling water to prevent the generation of the harmful substances; and a secondary treatment operation in which primarily treated gases passing through the primary treatment operation are submerged in treatment water containing a harmful gas treatment agent dissolved therein, and thus residual substances are treated.
  • the primary treatment operation may further include an operation in which the harmful gases introduced therein pass through rotary blades rotated in a submerged state under the cooling water, and thus are discharged in the form of microbubbles into the cooling water.
  • the apparatus for preventing the generation of the harmful substances by harmful gases according to the present invention can fundamentally prevent the generation of the harmful substances such as dioxins through the pure cooling water, in which a chemical component is not added, using heat, and thus can prevent the generation moment of the harmful substances. Also, the residual harmful substances which are not treated in the primary prevention processing part can be removed and collected in the secondary prevention processing part through the treatment water, and thus the emission of the harmful substances can be completely prevented.
  • the processing chamber and the rotary blades are additionally provided at the moving path of the harmful gases and the harmful substances, the entire structure is simple, and thus the costs for installation and management can be reduced. That is, since a separate facility for collecting and storing the dioxins is not required, the management cost can be reduced, comparing with the related art.
  • the primary prevention processing part and the secondary prevention processing part can be selectively used according to the generation processes of the harmful gases and the harmful substances, management efficiency can be increased.
  • FIG. 1 is a schematic view schematically illustrating a structure of an apparatus 1 for treating harmful gases and preventing generation of and removing harmful substances according to an embodiment of the present invention.
  • An apparatus 1 for treating harmful gases and preventing generation of and removing harmful substances is installed to be connected with a flue 20 installed at steel mills, thermoelectric power plants, petrochemical plants, garbage incineration plants or the like to discharge the harmful substances into the atmosphere.
  • the apparatus 1 for treating the harmful gases and preventing the generation of and removing the harmful substances includes a primary prevention processing part 100 which rapidly cools harmful gases G1 by bringing them into contact with cooling water W and thus prevents the generation of the harmful substances, and a secondary prevention processing part 200 which purifies residual harmful substances once more by bringing primarily treated gases G2 treated in the primary prevention processing part 100 into contact with treatment water A, and thus processes the primarily treated gases G2 into secondarily treated gas G3 in the form of clean air which can be discharged into the atmosphere.
  • the primary prevention processing part 100 and the secondary prevention processing part 200 are installed and used as a set.
  • the secondary prevention processing part 200 may be selectively used.
  • the primary prevention processing part 100 and the secondary prevention processing part 200 may be used separately or together according to the type, concentration, temperature and generation process of the harmful gas.
  • the primary prevention processing part 100 includes a primary processing chamber 110 in which the cooling water W is stored, a primary suction pipe 120 which is connected with the flue 20 and suctions the harmful gases G1, a primary rotary blade part 130 which is connected with the primary suction pipe 120 and generates a suction pressure by rotation of rotary blades 137, a primary rotary blade driving part 140 which rotates the primary rotary blade part 130, and a cooling water circulation and filtration part 150 which circulates the cooling water W in the primary processing chamber 110.
  • the primary processing chamber 110 is formed in a closed housing shape, and accommodates the cooling water W therein.
  • the cooling water W is accommodated at a 1/3 height of the primary processing chamber 110.
  • a surface of the cooling water W is maintained horizontally.
  • the surface of the cooling water W is formed to be inclined by a centrifugal force, as indicated by W1 in FIG. 1 .
  • the flue 20 is inserted through an upper portion of the primary processing chamber 110, and the primary rotary blade driving part 140 is coupled to the primary rotary blade part 130 through a lower portion of the primary processing chamber 110.
  • the primary suction pipe 120 connects the flue 20 with the primary rotary blade part 130, and enables the harmful gases G1 to be moved to the primary rotary blade part 130.
  • An upper area of the primary suction pipe 120 is inserted into the flue 20, and a lower area thereof is connected with a harmful gas suction pipe 135.
  • the primary suction pipe 120 is formed to be inserted from the harmful gas suction pipe 135 into the flue 20 to a predetermined height. It is preferable that an outer diameter of the primary suction pipe 120 is formed corresponding to an inner diameter of the flue 20, and thus all of the harmful gases G1 passed through the flue 20 are introduced into the primary suction pipe 120.
  • the primary rotary blade part 130 is rotated in a submerged state under the cooling water W, and serves to generate the suction pressure by which the harmful gases G1 are moved and to discharge the harmful gases G1 in the form of microbubbles into the cooling water W by a rotation force.
  • the primary rotary blade part 130 includes an upper support plate 131 and a lower support plate 133, the harmful gas suction pipe 135 which connects the upper support plate 131 and the lower support plate 133 with each other, and a plurality of rotary blades 137 which are coupled to an outer circumferential surface of the harmful gas suction pipe 135 at regular intervals.
  • the harmful gas suction pipe 135 is coupled to a lower end of the primary suction pipe 120, and moves the harmful gases moved through the primary suction pipe 120 toward the plurality of rotary blades 137.
  • Harmful gas discharge ports 135a are formed at the outer circumferential surface of the harmful gas suction pipe 135 to be spaced apart from each other at regular intervals in a lengthwise direction.
  • Each of the harmful gas discharge ports 135a is formed through between one pair of adjacent rotary blades 137, and discharges the harmful gases G1 between the rotary blades 137.
  • the upper support plate 131 and the lower support plate 133 are coupled to an upper end and a lower end of the harmful gas suction pipe 135, respectively, and cover upper and lower sides of the plurality of rotary blades 137. Therefore, the harmful gases G1 discharged through the harmful gas discharge ports 135a may not escape to an outside, and may be introduced into the cooling water W between the rotary blades 137.
  • the upper support plate 131 and the lower support plate 133 cover a moving path of the rotary blades 137 by a side connection plate 134. Therefore, when the cooling water W in which the harmful gases G1 are dissolved is discharged between the rotary blades 137, the side connection plate 134 may prevent the cooling water W from being introduced again from an outside and obstructing a flow of the discharged cooling water W.
  • the plurality of rotary blades 137 are rotatably formed to spirally extend from the outer circumferential surface of the harmful gas suction pipe 135.
  • the rotary blades 137 receive a driving force from the primary rotary blade driving part 140, and are rotated.
  • the primary rotary blade driving part 140 is connected to the harmful gas suction pipe 135 to rotate the harmful gas suction pipe 135 and thus to drive the plurality of rotary blades 137.
  • the rotary blades 137 may be formed to spirally extend, as illustrated in the drawing, or may be radially formed in a linear shape. At this time, a protrusion end 137a which protrudes with a predetermined length 1 to an outside of each of the upper support plate 131 and the lower support plate 133 is formed at an end area of each rotary blade 137.
  • the protrusion end 137a Since the protrusion end 137a protrudes to the outside of each of the upper support plate 131 and the lower support 133, the protrusion end 137a is directly in contact with the cooling water W. Therefore, when the rotary blades 137 are rotated, the protrusion end 137a receives a great pressure, while colliding with the cooling water W.
  • the protrusion end 137a is formed to have an angle ⁇ 2 larger than an angle ⁇ 1 of each of the rotary blades 137 with respect to the harmful gas suction pipe 135. That is, the protrusion end 137a is formed to be bent from an end of each of the rotary blades 137 at a larger angle.
  • the harmful gases G1 collide with the rotary blades 137 so that pressure is applied when being discharged between the rotary blades 137, the harmful gases G1 are dissolved in the cooling water W in the form of microbubbles.
  • the harmful gases generated in an incinerator 10 typically contain harmful substances having a high temperature of about 900 °C or more.
  • they are decomposed at a high temperature of 850 °C, and are maximally produced at a temperature of 320 to 390 °C.
  • the harmful gases G1 in the form of microbubbles dissolved in the cooling water W between the rotary blades 137 are rapidly cooled from the temperature of 900 °C to reach a temperature of 100 °C. Therefore, a period of time while the harmful gases G1 remain in a temperature span of 320 to 380 °C at which the dioxins are generated is only about 1 second. Accordingly, the harmful substances such as the dioxins are fundamentally prevented from being generated from the harmful gases G1.
  • the primary prevention processing part 100 fundamentally prevents the generation of the harmful substances such as the dioxins, a conventional process for collecting, storing and managing previously generated harmful substances is not required.
  • the cooling water circulation and filtration part 150 is provided at one side of the primary processing chamber 110 to circulate the cooling water W heat-exchanged with the high temperature harmful gases G1. At this time, dust or the like is dissolved in the cooling water, while being in contact with the harmful gases G1 in the primary processing chamber 110.
  • the cooling water circulation and filtration part 150 includes a circulation pipe 151 which circulates the cooling water W, a circulation pump 152, and a filtration part 153 which filters harmful substances, such as sludge, contained in the cooling water W. Also, if necessary, the cooling water circulation and filtration part 150 may further include a cooling part (not shown) which maintains the cooling water at a proper temperature.
  • the secondary prevention processing part 200 is connected to the primary processing chamber 110 and a primary treated gas discharge pipe 211.
  • the secondary prevention processing part 200 serves to purify and discharge the primarily treated gases G2, in which the generation of the harmful gases is prevented but residual harmful substances are contained, to the atmosphere.
  • the secondary prevention processing part 200 has the same mechanical configuration as the primary prevention processing part 100, but is different from the primary prevention processing part 100 in that treatment water A is stored therein.
  • the primary prevention processing part 100 accommodates the cooling water W to rapidly cool the harmful gases G1, but the secondary prevention processing part 200 accommodates the treatment water A.
  • the treatment water A serves to remove, neutralize and collect residual air pollutants contained in the primarily treated gases G2.
  • the treatment water A is produced by dissolving a harmful gas treatment agent in water.
  • the harmful gas treatment agent may be differently provided according to the type of the harmful gas to be treated.
  • liquid sodium hydroxide is used as the harmful gas treatment agent.
  • a dissolution rate of the liquid sodium hydroxide may be set within a range of 3% to 10%.
  • Bubbles in the treatment water A are generated by rotation of a secondary rotary blade part 230 for treatment of the harmful gases.
  • the bubbles are discharged to an outside of a secondary processing chamber 210, purified in a purification part (not shown), and then collected or discharged after the purifying.
  • the harmful gases G1 produced by the flame F generated from the incinerator 10 are moved through the flue 20. At this time, an end of the flue 20 is connected with the primary suction pipe 120 of the primary prevention processing part 100.
  • the harmful gases G1 are discharged to the cooling water W along the inner surface of each of the rotary blades 137.
  • the harmful gases G1 are continuously in contact with the rotary blades 137 which are rotated at the high speed, and thus are converted into the microbubbles.
  • the harmful gases G1 in the form of the microbubbles are in contact with the cooling water W, and a dissolution rate thereof in the cooling water W is increased due to a wide contact area.
  • the harmful gases G1 in the form of the microbubbles are rapidly cooled within a few seconds due to a great temperature difference, and thus the generation of a harmful substance such as a dioxin is prevented.
  • the primarily treated gases G2 which are in contact with the cooling water W are moved to the secondary prevention processing part 200 through a secondarily treated gas duct 20.
  • the primarily treated gases G2 passed through a secondary suction pipe 220 and the secondary rotary blade part 230 reacts with the treatment water A in which the liquid sodium hydroxide is dissolved, and thus the residual substances are absorbed and collected, neutralized and removed.
  • Secondarily treated gases G3 which are secondarily treated like this are purified into a cleaned state which may be discharged into the atmosphere, and then discharged into the atmosphere through a secondarily treated gas discharge pipe 213.
  • FIG. 4 is a graph indicating a concentration change in oxygen and carbon dioxide contained in the harmful gases G1 at an inlet port M of the flue 20 by time
  • FIG. 5 is a table analyzing components of oxygen, carbon dioxide, carbon monoxide, nitrogen oxide and sulfur oxide contained in the secondarily treated gases G3 discharged through the secondarily treated gas discharge pipe 213 of FIG. 1 by time
  • FIG. 6 is a view illustrating the table of FIG. 5 indicated in a graph.
  • FIG. 7 is a graph indicating a concentration distribution of a substituted isomer in the harmful gases G1 at the inlet port M of the flue 20
  • FIG. 8 is a graph indicating the concentration distribution of the substituted isomer in the secondarily treated gases G3 flowing through the secondarily treated gas discharge pipe 213.
  • a combustion test in which household garbage is burnt in the incinerator 10 using one primary prevention processing part 100 was carried out, and concentrations of the harmful substances were measured for four hours by a qualified measuring organization.
  • a discharge concentration of the dioxins at the inlet port M of the flue 20 was 20.68ng-TEQ/Nm 2
  • the discharge concentration of the dioxins was 2.98ng-TEQ/Nm 2
  • an average discharge concentration of the nitrogen oxide was 27.2ppm
  • the discharge concentration of the sulfur oxide was ppm. Accordingly, it may be understood that removal efficiency of the dioxins between the measured positions is about 85.6%, and the generation of the harmful substances is generally reduced.
  • the apparatus for treating the harmful gases and preventing the generation of and removing the harmful substances according to the present invention may fundamentally prevent the generation of the harmful substances such as the dioxin through the pure cooling water, in which a chemical component is not added, using heat, and thus can prevent the generation moment of the harmful substances. Also, the harmful substances remaining in the primarily treated gas may be removed and collected again in the secondary prevention processing part through the treatment water, and thus the emission of the harmful substances can be completely prevented.
  • the processing chamber and the rotary blades are additionally provided at the moving path of the harmful gases and the harmful substances, the entire structure is simple, and thus the costs for installation and management may be reduced. That is, since a separate facility for collecting and storing the dioxins is not required, the management cost can be reduced, compared with the related art.
  • the primary prevention processing part and the secondary prevention processing part may be selectively used according to the generation processes of the harmful gases and the harmful substances, management efficiency may be increased.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Environmental & Geological Engineering (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Biomedical Technology (AREA)
  • Health & Medical Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Treating Waste Gases (AREA)
  • Gas Separation By Absorption (AREA)
  • Chimneys And Flues (AREA)

Abstract

The present invention relates to an apparatus for treating harmful gases and preventing the generation of and removing harmful substances, comprising a primary prevention processing part, which is connected to a flue through which harmful gases generated due to high-temperature flame flow, for quenching the harmful gases and thereby preventing harmful substances from generating from the harmful gases. The primary prevention processing part comprises: a primary processing chamber in which cooling water is accommodated; a primary suction pipe provided inside the primary processing chamber and connected to the flue; a primary rotating blade part, which is connected to the lower part of the primary suction pipe, and which rotates submerged under the cooling water so as to emit the harmful gases in the form of microbubbles into the cooling water and thereby allow the harmful gases to come into contact with the cooling water and be quenched; and a primary blade rotating part for rotating the primary rotating blade part.

Description

    Technical Field
  • This invention relates to an apparatus and method for treating harmful gases and preventing generation of and removing harmful substances, and more particularly, to an apparatus and method for treating harmful gases and preventing generation of and removing harmful substances, which rapidly cools the harmful gases and thus fundamentally prevents the generation of and removes harmful substances such as dioxins.
    • Background Art
  • Exhaust gases generated from an incinerator which incinerates household garbage of cities or industrial waste contain harmful substances such as CO2, HCl, NOx, Sox, dust and dioxins. Various conventional methods for treating the exhaust gases containing the above-described harmful substances have been used.
  • Most current methods for preventing emission of the harmful substances have a system for collecting and managing the harmful substances after the harmful substances are generated. That is, the current methods have a technical system which maximally collects the harmful substances, by generating the harmful substances. Therefore, since the harmful substances are generated somewhere, and the generated substances should be collected and stored, there is a problem in management thereof.
  • Also, currently commercialized apparatuses for removing and collecting the harmful substances require an injection type cooling tower or separate facilities and devices for forming cooled air to cool a high temperature generated at a site. Accordingly, there are some problems that a wide installation area and equipment for installing the facilities are required, and high costs are involved in installation and management of the facilities.
  • Such conventional technologies for preventing emission of the harmful substances cause many problems such as the wide installation area due to an increase in a size of a facility for preventing the emission of the harmful substances and high investment costs. The high costs cause a rise in manufacturing cost, and thus lead to a serious problem in price competitiveness of production goods, and particularly, provide a big worry to many companies which are confronted with regulations relative to greenhouse gas emission.
    • [Related technical documents] [Patent documents]
    • (Patent document 1) Korean Patent No.10-0613303 entitled "Hybrid-Type Method and Apparatus for Treating Exhaust Gas"
    • (Patent document 2) Korean Patent No.10-1133206 entitled "Charcoal Ignition Device with Harmful Material Removal Function"
    Summary of Invention Technical Problem
  • The present invention is directed to providing an apparatus and method for treating harmful gases and preventing generation of and removing harmful substances, which fundamentally prevents generation of harmful substances from harmful gases, and thus simplifies a harmful gas treatment process.
  • Also, the present invention is directed to providing an apparatus and method for treating harmful gases and preventing generation of and removing harmful substances, which has a simple structure and thus minimizes costs for installation and management of a facility.
  • Also, the present invention is directed to providing an apparatus and method for treating harmful gases and preventing generation of and removing harmful substances, which is able to prevent the generation of the harmful substances by rapidly cooling high temperature harmful gases, and also, to prevent the generation of the harmful substances from the harmful gases, which does not have high temperature, through treatment water, and thus to be selectively used according to a generation process of the harmful gases.
  • These objects and various advantages of the present invention will become apparent to those skilled in the art from the following exemplary embodiments of the present invention.
    • Solution to Problem
  • One aspect of the present invention provides an apparatus and method for treating harmful gases and preventing generation of and removing harmful substances, including a primary prevention processing part connected with a flue in which harmful gases and harmful substances generated by high temperature flame flow and configured to rapidly cool the harmful gases to prevent the harmful substances from being produced from the harmful gases, wherein the primary prevention processing part includes a primary processing chamber in which cooling water is accommodated; a primary suction pipe which is provided inside the primary processing chamber and connected with the flue; a primary rotary blade part which is coupled to a lower portion of the primary suction pipe, rotated in a submerged state under the cooling water, discharges the harmful gases in the form of microbubbles into the cooling water to allow the harmful gases to come into contact with the cooling water and to be rapidly cooled; and a primary rotary blade driving part which rotates the primary rotary blade part.
  • The primary suction pipe may be formed to have an outer diameter corresponding to an inner diameter of the flue, and may be provided so that an upper end thereof is inserted into the flue to a predetermined length and a lower end thereof is in communication with the primary rotary blade part.
  • The primary rotary blade part may include a harmful gas suction pipe where an upper portion is opened so as to be in communication with the primary suction pipe, and an outer circumferential surface having harmful gas discharge ports formed at regular intervals; an upper support plate and a lower support plate which are coupled to an upper portion and a lower portion of the harmful gas suction pipe, respectively; and a plurality of rotary blades which are spirally coupled at one sides of the harmful gas discharge ports and discharge the harmful gases to the cooling water.
  • Ends of the rotary blade may be formed to protrude outward to a predetermined length in radial directions of the upper support plate and the lower support plate.
  • A cooling water circulation and filtration part which circulates the cooling water therein and discharges sludge is provided at one side of the primary processing chamber.
  • The apparatus may further include a secondary prevention processing part which dissolves primarily treated gases treated in the primary prevention processing part in treatment water in which a harmful gas treatment agent dissolved, and treats residual substances contained in the primarily treated gases.
  • Meanwhile, the object of the present invention can be achieved by the apparatus and method for treating the harmful gases and preventing the generation of and removing the harmful substances. Another aspect of the present invention provides a method for treating harmful gases and preventing generation of and removing harmful substances, including a primary treatment operation in which the apparatus for treating the harmful gases and preventing the generation of and removing the harmful substances is coupled to a flue in which the high temperature harmful gases flow, rapidly cools the harmful gases by bringing the harmful gases into contact with cooling water to prevent the generation of the harmful substances; and a secondary treatment operation in which primarily treated gases passing through the primary treatment operation are submerged in treatment water containing a harmful gas treatment agent dissolved therein, and thus residual substances are treated.
  • The primary treatment operation may further include an operation in which the harmful gases introduced therein pass through rotary blades rotated in a submerged state under the cooling water, and thus are discharged in the form of microbubbles into the cooling water.
    • Advantageous Effects of Invention
  • The apparatus for preventing the generation of the harmful substances by harmful gases according to the present invention can fundamentally prevent the generation of the harmful substances such as dioxins through the pure cooling water, in which a chemical component is not added, using heat, and thus can prevent the generation moment of the harmful substances. Also, the residual harmful substances which are not treated in the primary prevention processing part can be removed and collected in the secondary prevention processing part through the treatment water, and thus the emission of the harmful substances can be completely prevented.
  • Also, since the processing chamber and the rotary blades are additionally provided at the moving path of the harmful gases and the harmful substances, the entire structure is simple, and thus the costs for installation and management can be reduced. That is, since a separate facility for collecting and storing the dioxins is not required, the management cost can be reduced, comparing with the related art.
  • Also, since the primary prevention processing part and the secondary prevention processing part can be selectively used according to the generation processes of the harmful gases and the harmful substances, management efficiency can be increased.
    • Brief Description of Drawings
    • FIG. 1 is a schematic view schematically illustrating an entire structure of an apparatus for treating harmful gases and preventing generation of and removing harmful substances according to the present invention.
    • FIG. 2 is a perspective view illustrating a structure of a rotary blade part of the apparatus for treating the harmful gases and preventing the generation of and removing the harmful substances according to the present invention.
    • FIG. 3 is a plan view illustrating a planar structure of the rotary blade part of the apparatus for treating the harmful gases and preventing the generation of and removing the harmful substances according to the present invention.
    • FIGS. 4 to 8 are a table and graphs illustrating treatment results of the harmful gases through the apparatus for treating the harmful gases and preventing the generation of and removing the harmful substances according to the present invention.
    Detailed Description of Embodiment
  • Hereinafter, exemplary embodiments of the present invention will be described with reference to the accompanying drawings to provide a sufficient understanding of the present invention. However, the present invention is not limited to the exemplary embodiments disclosed below, but can be modified in various forms. The following exemplary embodiments are described in order to enable those of ordinary skill in the art to embody and practice the invention. Therefore, sizes and shapes of construction elements shown in the drawings may be exaggeratedly illustrated for the sake of convenience and clarity. In each of the drawings, the same components may be designated by the same reference numerals. In the following description, if it is considered that the specific description of the related and noticed functions or structures may obscure the gist of the present invention, the specific description will be omitted.
  • FIG. 1 is a schematic view schematically illustrating a structure of an apparatus 1 for treating harmful gases and preventing generation of and removing harmful substances according to an embodiment of the present invention.
  • An apparatus 1 for treating harmful gases and preventing generation of and removing harmful substances according to an embodiment of the present invention is installed to be connected with a flue 20 installed at steel mills, thermoelectric power plants, petrochemical plants, garbage incineration plants or the like to discharge the harmful substances into the atmosphere.
  • The apparatus 1 for treating the harmful gases and preventing the generation of and removing the harmful substances includes a primary prevention processing part 100 which rapidly cools harmful gases G1 by bringing them into contact with cooling water W and thus prevents the generation of the harmful substances, and a secondary prevention processing part 200 which purifies residual harmful substances once more by bringing primarily treated gases G2 treated in the primary prevention processing part 100 into contact with treatment water A, and thus processes the primarily treated gases G2 into secondarily treated gas G3 in the form of clean air which can be discharged into the atmosphere.
  • Here, in smokestack industries, such as the steel mills, the thermoelectric power plants, the petrochemical plants and the garbage incineration plants, in which the high temperature harmful gases or harmful substances are generated by flame F, the primary prevention processing part 100 and the secondary prevention processing part 200 are installed and used as a set.
  • However, in other industries, such as IT-related industries, high precision industries, industries requiring clean air, industries suffering from yellow dust, construction sites and large buildings, in which the harmful gases or harmful substances are generated without generation of the flame, only the secondary prevention processing part 200 may be selectively used.
  • That is, the primary prevention processing part 100 and the secondary prevention processing part 200 may be used separately or together according to the type, concentration, temperature and generation process of the harmful gas.
  • The primary prevention processing part 100 includes a primary processing chamber 110 in which the cooling water W is stored, a primary suction pipe 120 which is connected with the flue 20 and suctions the harmful gases G1, a primary rotary blade part 130 which is connected with the primary suction pipe 120 and generates a suction pressure by rotation of rotary blades 137, a primary rotary blade driving part 140 which rotates the primary rotary blade part 130, and a cooling water circulation and filtration part 150 which circulates the cooling water W in the primary processing chamber 110.
  • The primary processing chamber 110 is formed in a closed housing shape, and accommodates the cooling water W therein. The cooling water W is accommodated at a 1/3 height of the primary processing chamber 110. When the primary rotary blade part 130 is not rotated, a surface of the cooling water W is maintained horizontally. When the primary rotary blade part 130 is rotated, the surface of the cooling water W is formed to be inclined by a centrifugal force, as indicated by W1 in FIG. 1.
  • The flue 20 is inserted through an upper portion of the primary processing chamber 110, and the primary rotary blade driving part 140 is coupled to the primary rotary blade part 130 through a lower portion of the primary processing chamber 110.
  • The primary suction pipe 120 connects the flue 20 with the primary rotary blade part 130, and enables the harmful gases G1 to be moved to the primary rotary blade part 130. An upper area of the primary suction pipe 120 is inserted into the flue 20, and a lower area thereof is connected with a harmful gas suction pipe 135.
  • The primary suction pipe 120 is formed to be inserted from the harmful gas suction pipe 135 into the flue 20 to a predetermined height. It is preferable that an outer diameter of the primary suction pipe 120 is formed corresponding to an inner diameter of the flue 20, and thus all of the harmful gases G1 passed through the flue 20 are introduced into the primary suction pipe 120.
  • The primary rotary blade part 130 is rotated in a submerged state under the cooling water W, and serves to generate the suction pressure by which the harmful gases G1 are moved and to discharge the harmful gases G1 in the form of microbubbles into the cooling water W by a rotation force.
  • The primary rotary blade part 130 includes an upper support plate 131 and a lower support plate 133, the harmful gas suction pipe 135 which connects the upper support plate 131 and the lower support plate 133 with each other, and a plurality of rotary blades 137 which are coupled to an outer circumferential surface of the harmful gas suction pipe 135 at regular intervals.
  • The harmful gas suction pipe 135 is coupled to a lower end of the primary suction pipe 120, and moves the harmful gases moved through the primary suction pipe 120 toward the plurality of rotary blades 137. Harmful gas discharge ports 135a are formed at the outer circumferential surface of the harmful gas suction pipe 135 to be spaced apart from each other at regular intervals in a lengthwise direction. Each of the harmful gas discharge ports 135a is formed through between one pair of adjacent rotary blades 137, and discharges the harmful gases G1 between the rotary blades 137.
  • The upper support plate 131 and the lower support plate 133 are coupled to an upper end and a lower end of the harmful gas suction pipe 135, respectively, and cover upper and lower sides of the plurality of rotary blades 137. Therefore, the harmful gases G1 discharged through the harmful gas discharge ports 135a may not escape to an outside, and may be introduced into the cooling water W between the rotary blades 137.
  • The upper support plate 131 and the lower support plate 133 cover a moving path of the rotary blades 137 by a side connection plate 134. Therefore, when the cooling water W in which the harmful gases G1 are dissolved is discharged between the rotary blades 137, the side connection plate 134 may prevent the cooling water W from being introduced again from an outside and obstructing a flow of the discharged cooling water W.
  • The plurality of rotary blades 137 are rotatably formed to spirally extend from the outer circumferential surface of the harmful gas suction pipe 135. The rotary blades 137 receive a driving force from the primary rotary blade driving part 140, and are rotated. At this time, the primary rotary blade driving part 140 is connected to the harmful gas suction pipe 135 to rotate the harmful gas suction pipe 135 and thus to drive the plurality of rotary blades 137.
  • The rotary blades 137 may be formed to spirally extend, as illustrated in the drawing, or may be radially formed in a linear shape. At this time, a protrusion end 137a which protrudes with a predetermined length 1 to an outside of each of the upper support plate 131 and the lower support plate 133 is formed at an end area of each rotary blade 137.
  • Since the protrusion end 137a protrudes to the outside of each of the upper support plate 131 and the lower support 133, the protrusion end 137a is directly in contact with the cooling water W. Therefore, when the rotary blades 137 are rotated, the protrusion end 137a receives a great pressure, while colliding with the cooling water W. The protrusion end 137a is formed to have an angle θ2 larger than an angle θ1 of each of the rotary blades 137 with respect to the harmful gas suction pipe 135. That is, the protrusion end 137a is formed to be bent from an end of each of the rotary blades 137 at a larger angle.
  • As enlargedly illustrated in FIG. 3, when the rotary blades 137 are rotated clockwise, a great pressure P2 is applied to an outer surface of the protrusion end 137a, while the outer surface of the protrusion end 137a collides with the cooling water W, and a negative pressure P1 is applied to an inner surface of the protrusion end 137a. Therefore, the harmful gases G1 are discharged along inner surfaces of the rotary blades 137, and then dissolved in the cooling water W.
  • Meanwhile, since the harmful gases G1 collide with the rotary blades 137 so that pressure is applied when being discharged between the rotary blades 137, the harmful gases G1 are dissolved in the cooling water W in the form of microbubbles.
  • Here, the harmful gases generated in an incinerator 10 typically contain harmful substances having a high temperature of about 900 °C or more. In the case of dioxins, they are decomposed at a high temperature of 850 °C, and are maximally produced at a temperature of 320 to 390 °C.
  • The harmful gases G1 in the form of microbubbles dissolved in the cooling water W between the rotary blades 137 are rapidly cooled from the temperature of 900 °C to reach a temperature of 100 °C. Therefore, a period of time while the harmful gases G1 remain in a temperature span of 320 to 380 °C at which the dioxins are generated is only about 1 second. Accordingly, the harmful substances such as the dioxins are fundamentally prevented from being generated from the harmful gases G1.
  • That is, since the primary prevention processing part 100 according to the present invention fundamentally prevents the generation of the harmful substances such as the dioxins, a conventional process for collecting, storing and managing previously generated harmful substances is not required.
  • Meanwhile, the cooling water circulation and filtration part 150 is provided at one side of the primary processing chamber 110 to circulate the cooling water W heat-exchanged with the high temperature harmful gases G1. At this time, dust or the like is dissolved in the cooling water, while being in contact with the harmful gases G1 in the primary processing chamber 110. The cooling water circulation and filtration part 150 includes a circulation pipe 151 which circulates the cooling water W, a circulation pump 152, and a filtration part 153 which filters harmful substances, such as sludge, contained in the cooling water W. Also, if necessary, the cooling water circulation and filtration part 150 may further include a cooling part (not shown) which maintains the cooling water at a proper temperature.
  • Meanwhile, the secondary prevention processing part 200 is connected to the primary processing chamber 110 and a primary treated gas discharge pipe 211. The secondary prevention processing part 200 serves to purify and discharge the primarily treated gases G2, in which the generation of the harmful gases is prevented but residual harmful substances are contained, to the atmosphere.
  • The secondary prevention processing part 200 has the same mechanical configuration as the primary prevention processing part 100, but is different from the primary prevention processing part 100 in that treatment water A is stored therein. The primary prevention processing part 100 accommodates the cooling water W to rapidly cool the harmful gases G1, but the secondary prevention processing part 200 accommodates the treatment water A.
  • The treatment water A serves to remove, neutralize and collect residual air pollutants contained in the primarily treated gases G2. The treatment water A is produced by dissolving a harmful gas treatment agent in water. The harmful gas treatment agent may be differently provided according to the type of the harmful gas to be treated. However, in the embodiment of the present invention, liquid sodium hydroxide is used as the harmful gas treatment agent. A dissolution rate of the liquid sodium hydroxide may be set within a range of 3% to 10%.
  • Bubbles in the treatment water A are generated by rotation of a secondary rotary blade part 230 for treatment of the harmful gases. The bubbles are discharged to an outside of a secondary processing chamber 210, purified in a purification part (not shown), and then collected or discharged after the purifying.
  • An operation procedure of the apparatus 1 for treating the harmful gases and preventing the generation of and removing the harmful substances according to the present invention having the above-described structure will be described with reference to FIGS. 1 to 3.
  • The harmful gases G1 produced by the flame F generated from the incinerator 10 are moved through the flue 20. At this time, an end of the flue 20 is connected with the primary suction pipe 120 of the primary prevention processing part 100.
  • When the primary rotary blade part 130 is rotated by the primary rotary blade driving part 140, a negative pressure is formed in the primary suction pipe 120, and the harmful gases G1 are suctioned into the primary suction pipe 120. The harmful gases G1 suctioned into the primary suction pipe 120 are discharged through the harmful gas discharge ports 135a, and moved to between the adjacent rotary blades 137.
  • At this time, while the rotary blades 137 are rotated at high speed, the great pressure P2 is generated at an outer surface of each of the rotary blades 137, and the relatively small pressure P1 is generated at an inner surface thereof, and thus the harmful gases G1 are discharged to the cooling water W along the inner surface of each of the rotary blades 137. In this process, the harmful gases G1 are continuously in contact with the rotary blades 137 which are rotated at the high speed, and thus are converted into the microbubbles. The harmful gases G1 in the form of the microbubbles are in contact with the cooling water W, and a dissolution rate thereof in the cooling water W is increased due to a wide contact area. Also, the harmful gases G1 in the form of the microbubbles are rapidly cooled within a few seconds due to a great temperature difference, and thus the generation of a harmful substance such as a dioxin is prevented.
  • The primarily treated gases G2 which are in contact with the cooling water W are moved to the secondary prevention processing part 200 through a secondarily treated gas duct 20. The primarily treated gases G2 passed through a secondary suction pipe 220 and the secondary rotary blade part 230 reacts with the treatment water A in which the liquid sodium hydroxide is dissolved, and thus the residual substances are absorbed and collected, neutralized and removed. Secondarily treated gases G3 which are secondarily treated like this are purified into a cleaned state which may be discharged into the atmosphere, and then discharged into the atmosphere through a secondarily treated gas discharge pipe 213.
  • FIG. 4 is a graph indicating a concentration change in oxygen and carbon dioxide contained in the harmful gases G1 at an inlet port M of the flue 20 by time, FIG. 5 is a table analyzing components of oxygen, carbon dioxide, carbon monoxide, nitrogen oxide and sulfur oxide contained in the secondarily treated gases G3 discharged through the secondarily treated gas discharge pipe 213 of FIG. 1 by time, and FIG. 6 is a view illustrating the table of FIG. 5 indicated in a graph.
  • Also, FIG. 7 is a graph indicating a concentration distribution of a substituted isomer in the harmful gases G1 at the inlet port M of the flue 20, and FIG. 8 is a graph indicating the concentration distribution of the substituted isomer in the secondarily treated gases G3 flowing through the secondarily treated gas discharge pipe 213.
  • As illustrated in the drawings, a combustion test in which household garbage is burnt in the incinerator 10 using one primary prevention processing part 100 was carried out, and concentrations of the harmful substances were measured for four hours by a qualified measuring organization. As a result, a discharge concentration of the dioxins at the inlet port M of the flue 20 was 20.68ng-TEQ/Nm2, and in the primary treated gas discharge pipe 211, the discharge concentration of the dioxins was 2.98ng-TEQ/Nm2, an average discharge concentration of the nitrogen oxide was 27.2ppm, and the discharge concentration of the sulfur oxide was ppm. Accordingly, it may be understood that removal efficiency of the dioxins between the measured positions is about 85.6%, and the generation of the harmful substances is generally reduced.
  • As described above, the apparatus for treating the harmful gases and preventing the generation of and removing the harmful substances according to the present invention may fundamentally prevent the generation of the harmful substances such as the dioxin through the pure cooling water, in which a chemical component is not added, using heat, and thus can prevent the generation moment of the harmful substances. Also, the harmful substances remaining in the primarily treated gas may be removed and collected again in the secondary prevention processing part through the treatment water, and thus the emission of the harmful substances can be completely prevented.
  • Also, since the processing chamber and the rotary blades are additionally provided at the moving path of the harmful gases and the harmful substances, the entire structure is simple, and thus the costs for installation and management may be reduced. That is, since a separate facility for collecting and storing the dioxins is not required, the management cost can be reduced, compared with the related art.
  • Also, since the primary prevention processing part and the secondary prevention processing part may be selectively used according to the generation processes of the harmful gases and the harmful substances, management efficiency may be increased.
  • It will be understood that the foregoing embodiment of the apparatus for treating the harmful gases and preventing the generation of and removing the harmful substances of the present invention is for illustrative purposes only, and that, for a person of ordinary skill in the art, various substitutions, alternations and changes can be made without departing from the technical spirit or the essential characteristics of the present invention. Therefore, the above-described embodiments are for illustrating and not to limit the scope of the claims. Therefore, the technical spirit of the present invention is determined by the claims, and it should be understood that the present invention comprises all of equivalents and substitutes included in the technical scope and spirit of the invention.
    • [Detailed Description of Main Elements]
    • 1: apparatus for treating harmful gases and preventing generation of and removing harmful substances
    • 100: primary prevention processing part
    • 110: primary processing chamber
    • 120: primary suction pipe
    • 130: primary rotary blade part
    • 131: upper support plate 133: lower support plate 135: harmful gas suction pipe
    • 135a: harmful gas discharge port
    • 137: rotary blade 137a: protrusion end
    • 140: primary rotary blade driving part
    • 150: cooling water circulation and filtration part
    • 151: cooling water circulation pipe
    • 152: circulation pump 153: filtration part
    • 200: secondary prevention processing part
    • 210: secondary processing chamber
    • 211: primarily treated gas discharge pipe
    • 213: secondarily treated gas discharge pipe
    • 220: secondary suction pipe
    • 230: secondary rotary blade part
    • 240: secondary rotary blade driving part

Claims (7)

  1. An apparatus for treating harmful gases and preventing generation of and removing harmful substances, comprising:
    a primary prevention processing part connected with a flue in which harmful gases and harmful substances generated by high temperature flame flow and configured to rapidly cool the harmful gases to prevent the harmful substances from being produced from the harmful gases,
    wherein the primary prevention processing part comprises a primary processing chamber in which cooling water is accommodated; a primary suction pipe which is provided inside the primary processing chamber and connected with the flue; a primary rotary blade part which is coupled to a lower portion of the primary suction pipe, rotated in a submerged state under the cooling water, discharges the harmful gases in the form of microbubbles into the cooling water to allow the harmful gases to come into contact with the cooling water and to be rapidly cooled; and a primary rotary blade driving part which rotates the primary rotary blade part.
  2. The apparatus of claim 1, wherein the primary suction pipe is formed to have an outer diameter corresponding to an inner diameter of the flue, and provided so that an upper end thereof is inserted into the flue to a predetermined length and a lower end thereof is in communication with the primary rotary blade part.
  3. The apparatus of claim 2, wherein the primary rotary blade part comprises a harmful gas suction pipe where an upper portion is opened so as to be in communication with the primary suction pipe, and an outer circumferential surface having harmful gas discharge ports formed at regular intervals; an upper support plate and a lower support plate which are coupled to an upper portion and a lower portion of the harmful gas suction pipe, respectively; and a plurality of rotary blades which are spirally coupled at one sides of the harmful gas discharge ports and discharge the harmful gases to the cooling water.
  4. The apparatus of claim 3, wherein ends of the rotary blades are formed to protrude outward to a predetermined length in radial directions of the upper support plate and the lower support plate.
  5. The apparatus of claim 4, wherein a cooling water circulation and filtration part which circulates the cooling water therein is provided at one side of the primary processing chamber.
  6. The apparatus of any one of claims 1 to 5, further comprising a secondary prevention processing part which dissolves primarily treated gases treated in the primary prevention processing part in treatment water in which a harmful gas treatment agent dissolved, and treats residual substances contained in the primarily treated gases.
  7. A method for treating harmful gases and preventing generation of and removing harmful substances using the apparatus for treating the harmful gases and preventing the generation of and removing the harmful substances of claim 1, further comprising:
    a primary treatment operation in which the apparatus for treating the harmful gases and preventing the generation of and removing the harmful substances is coupled to a flue in which the high temperature harmful gases flow, rapidly cools the harmful gases by bringing the harmful gases into contact with cooling water, and thus prevents the generation of the harmful substances; and
    a secondary treatment operation in which primarily treated gases passing through the primary treatment operation are submerged in treatment water containing a harmful gas treatment agent dissolved therein, and thus residual substances are treated,
    wherein the primary treatment operation comprises an operation in which the harmful gases introduced therein pass through rotary blades rotated in a submerged state under the cooling water, and thus are discharged in the form of microbubbles into the cooling water.
EP14810303.9A 2013-06-11 2014-05-07 Apparatus and method for treating harmful gases and preventing generation of and removing harmful substances Withdrawn EP3009180A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
KR1020130066525A KR101344658B1 (en) 2013-06-11 2013-06-11 Eliminaing device for removing poisonous substance of noxious gases and method therof
PCT/KR2014/003999 WO2014200184A1 (en) 2013-06-11 2014-05-07 Apparatus and method for treating harmful gases and preventing generation of and removing harmful substances

Publications (1)

Publication Number Publication Date
EP3009180A1 true EP3009180A1 (en) 2016-04-20

Family

ID=49989052

Family Applications (1)

Application Number Title Priority Date Filing Date
EP14810303.9A Withdrawn EP3009180A1 (en) 2013-06-11 2014-05-07 Apparatus and method for treating harmful gases and preventing generation of and removing harmful substances

Country Status (6)

Country Link
US (1) US20160121256A1 (en)
EP (1) EP3009180A1 (en)
JP (1) JP2016523699A (en)
KR (1) KR101344658B1 (en)
CN (1) CN105492104A (en)
WO (1) WO2014200184A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107174920A (en) * 2017-07-30 2017-09-19 合肥杰代机电科技有限公司 A kind of activated carbon fiber organic waste gas adsorption/desorption cleaning equipment

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105498404A (en) * 2016-01-15 2016-04-20 郝轩胜 Novel environment-friendly coal fired boiler
CN108224552A (en) * 2016-12-22 2018-06-29 王支业 A kind of air purifier
CN109990407B (en) * 2019-04-10 2021-07-02 湖南匡为科技有限公司 Water smoke air purification device
CN111167295A (en) * 2020-01-15 2020-05-19 邓智超 Acid gas purification device for underground engineering construction
CN113413706B (en) * 2021-07-09 2022-12-13 江苏科技大学 Dust treatment device of plasma cutting machine
CN114814075B (en) * 2022-04-02 2024-03-26 南京理工大学北方研究院 Testing device for harmful gas generated by combustion of high polymer material
CN115006978B (en) * 2022-06-27 2023-03-24 安徽相恒气体科技有限公司 Acetylene gas tail gas recovery and purification device

Family Cites Families (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3756580A (en) * 1972-01-31 1973-09-04 Peabody Engineering Corp Gas washing apparatus
PL171012B1 (en) * 1993-07-08 1997-02-28 Waclaw Borszynski Wet combustion gas purification system for use advantageously in coal, cok4e and heating oil combustion processes
JP2739427B2 (en) * 1994-03-09 1998-04-15 株式会社タステム Underwater cooling system for high-temperature PCB exhaust gas
TW354364B (en) * 1997-03-27 1999-03-11 Ogawara Kakoki Kk Method for cooling the waste gas in the incinerator furnace and the device of the same
JPH10286435A (en) * 1997-04-16 1998-10-27 Tetsuto Tamura Quencher for prevention of resynthesis of dioxin
JP2003024739A (en) * 2001-07-16 2003-01-28 Kenichi Imako Deodorizing device of garbage treatment machine
JP2003144844A (en) * 2001-11-07 2003-05-20 Mitsubishi Heavy Ind Ltd Decomposing equipment for organic halogen compound
CN2595434Y (en) * 2003-01-20 2003-12-31 原跃 Swirl jet bubbling type dust removing desulfurizer
KR20040090042A (en) * 2003-04-16 2004-10-22 최기호 Collection appratus of air cleaner of water type injection
JP4382470B2 (en) * 2003-12-24 2009-12-16 義次 桜井 Waste pyrolysis treatment equipment
CN1559653A (en) * 2004-03-08 2005-01-05 李风仁 Smoke purifying device
KR100613303B1 (en) 2004-11-17 2006-08-21 이인섭 Hybrid-type method and apparatus for treating exhaust gas
CN1745880A (en) * 2005-08-15 2006-03-15 周宗云 Low-consumption and high-efficient smoke purifying system with desulfuring, deoiling, dust-proof and dust-collecting functions
CN102451610B (en) * 2010-10-15 2014-01-01 中国石油化工股份有限公司 Treatment method for nitrogen oxide tail gas discharged from industrial production furnace, and apparatus thereof
KR101133206B1 (en) 2011-08-08 2012-04-09 유명선 Charcoal fire with hazardous materials removal apparatus

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO2014200184A1 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107174920A (en) * 2017-07-30 2017-09-19 合肥杰代机电科技有限公司 A kind of activated carbon fiber organic waste gas adsorption/desorption cleaning equipment

Also Published As

Publication number Publication date
KR101344658B1 (en) 2013-12-24
WO2014200184A1 (en) 2014-12-18
JP2016523699A (en) 2016-08-12
US20160121256A1 (en) 2016-05-05
CN105492104A (en) 2016-04-13

Similar Documents

Publication Publication Date Title
EP3009180A1 (en) Apparatus and method for treating harmful gases and preventing generation of and removing harmful substances
KR100509304B1 (en) Method for processing perfluoride and apparatus for treating same
KR101453341B1 (en) Wet Scrubber Systme Combined With Electrostatic Induction
JP2018158330A (en) Waste gas treatment method applying nano-bubbles and treatment system of the same
KR101457814B1 (en) Gas filtration appratus and system
JP2007231869A (en) Exhaust emission control device
KR101645171B1 (en) NON-DEGRADABLE HAZARDOUS GAS PURIFICATION SYSTEM GENERATED IN THE SEMICONDUCTOR AND VOCs EMISSION PROCESS
JP5368003B2 (en) Filtration type dust collector and exhaust gas abatement system using the same
JP2007175617A (en) Method and apparatus for cleaning exhaust gas from incineration furnace
JP7485892B2 (en) Smoke treatment equipment
CN212914995U (en) Industrial waste gas circulation purification treatment device
KR102273029B1 (en) Exhaust gas wet treatment device to remove odor and dust
CN207126347U (en) A kind of efficient organic waste gas treatment system
JP3796618B2 (en) Purification method of flon combustion exhaust gas
WO2022210389A1 (en) Pollutant treatment system and pollutant treatment method
CN106039913A (en) Flue gas purifying system
CN211232932U (en) Flue gas heat exchanger and flue gas processing system
EP2653172A2 (en) Air conditioning apparatus and ion generator device
CN216572369U (en) Waste gas treatment device based on UV ultraviolet irradiation
Yamamoto et al. Wet type plasma reactor for incinerator
KR200291649Y1 (en) Condensing and heat system
JP2007032999A (en) Incineration system
KR200196779Y1 (en) Exhaust gas purification apparatus
CN213159946U (en) Waste gas purification treatment device for incineration waste gas tower
JP4901849B2 (en) Air purifier, analysis room, and air purification method

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 20151215

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

AX Request for extension of the european patent

Extension state: BA ME

RIN1 Information on inventor provided before grant (corrected)

Inventor name: KIM, WOONG HOE

DAX Request for extension of the european patent (deleted)
STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION HAS BEEN WITHDRAWN

18W Application withdrawn

Effective date: 20161013